Fuel cell separator and fuel cell stack and reactant gas control method thereof

ABSTRACT

A fuel cell separator, a fuel cell stack having the fuel cell separator, and a reactant gas control method of the fuel cell stack are provided. That is, even when the fuel cell stack operates under the low load operation condition, a reactant gas is supplied to the reactant gas passages of the fuel cell separator, and thus, the length of the passage can be shortened by 50% as compared with the prior art having only one reactant gas passage. Therefore, the reactant gas can be effectively supplied without experiencing pressure loss. Further, in the high load operation of the fuel cell stack, the reactant gas is introduced into the first reactant gas passage of the fuel cell separator and utilized in half of the whole electrode area. Subsequently, the reactant gas is introduced into the second reactant gas passage and utilized in the remaining half of the electrode area. The flow rate of the reactant gas flowing along the passage channels is increased by two times, even when the reactant gas utilizing rate is identical as compared with the reactant gas flow in the low load operation. As a result, the moisture existing in the passage channels can be more effectively discharged and the flooding phenomenon occurring in the high load operation can be prevented. By controlling the reactant gas supply in accordance with an operation condition of the fuel cell stack without experiencing pressure loss and deterioration of the utilizing rate, the flooding phenomenon and concentration polarization phenomenon that occur in the fuel cell stack can be prevented.

CROSS-REFERENCE TO RELATED APPLICATION

This application is a Divisional application of U.S. patent applicationSer. No. 12/067,086 filed on Mar. 17, 2008, which is a National Stageapplication of PCT/KR2007/002520 filed on May 23, 2007, which claimspriority to Korean Patent Application No. 10-2006-0080442 filed on Aug.24, 2006, which is incorporated herein by reference.

TECHNICAL FIELD

The present invention relates to a fuel cell stack using a protonexchange membrane fuel cell (PEMFC). More particularly, the presentinvention relates to a fuel cell separator that can maintain a highreactant gas utilizing rate and effectively control water generated byan electrochemical reaction even when an operation condition varies. Thepresent invention further relates to a fuel cell stack having the fuelcell separator, and a reactant gas control method of the fuel cellstack.

BACKGROUND ART

A PEMFC uses a proton exchange membrane having a hydrogen ion exchangeproperty as an electrolyte membrane. The PEMFC includes a pair ofelectrodes formed on opposite surfaces of the proton exchange membraneand a separator. The PEMFC generates electricity and heat through anelectrochemical reaction between a fuel gas containing hydrogen and aircontaining oxygen. The PEMFC has an excellent output property and aquick start capability and can be operated at a relatively lowtemperature. Therefore, the PEMFC has been widely used in variousapplications such as a portable power source, an automotive powersource, and a home cogeneration plant.

The electrodes used for the PEMFC include a catalyst layer containing asupported metal catalyst, such as platinum group metal, and a diffusionlayer formed on an outer surface of the catalyst layer and havingbreathable and electron conduction properties. The diffusion layer isgenerally formed of a carbon paper or a carbon non-woven fabric. Theassembly of the proton exchange membrane and the electrodes formed onopposite surfaces of the proton exchange membrane is referred to as “amembrane-electrode assembly (MEA)”. A conductive separator is installedon an outer side of the MEA to mechanically fix the electrodes andelectrically interconnect adjacent MEAs. The assembly of the conductiveseparator, the proton exchange membrane, and the electrodes is referredto as “a unit cell”.

A fluid passage is formed on the separator contacting the MEA to supplya reactant gas to an electrode surface and to deliver surplus gas and areaction by-product. The fluid passage may be separately prepared andinstalled on the separator. However, the fluid passage is generallyprovided in the form of a groove shape on a surface of the separator.

Particularly, cathode and anode separation plates of the fuel cellseparator require electric conduction, gas-tightness, andcorrosion-resistance characteristics. Therefore, in order to form thegroove, a method that forms the groove by cutting a resin-impregnatedgraphite plate, a method that forms the groove by compression-formingcarbon-compound powders, or a method that forms the groove by pressing ametal plate and coating a corrosion-resistance material on the metalplate has been used.

Further, the PEMFC includes a cooling unit along which a coolant flowsand which is installed for one through three unit cells to dissipateheat generated by the operation thereof. The cooling unit includes afuel gas separation plate having a first surface provided with a fuelgas passage and a second surface provided with a coolant passage, and anoxidizing gas separation plate having a first surface provided with anoxidizing gas passage and a second surface provided with a coolantpassage. The fuel gas separation plate is assembled with the oxidizinggas separation plate such that the coolant passage surface (the secondsurface) of the fuel gas separation plate contacts the coolant passagesurface (the second surface) of the oxidizing gas separation plate.Alternatively, the cooling unit may include a fuel gas separation platehaving a first surface provided with a fuel gas passage and a secondsurface (an even surface) that is not provided with any passage, and anoxidizing gas separation plate having a first surface provided with anoxidizing gas passage and a second surface (a coolant passage surface)provided with a coolant passage. The fuel gas separation plate isassembled with the oxidizing gas separation plate such that the evensurface (the second surface) of the fuel gas separation plate contactsthe coolant passage surface (the second surface) of the oxidizing gasseparation plate.

The separation plate of the PEMFC is provided with at least two throughholes for each of the fuel gas, the oxidizing gas, and the coolant.Then, by connecting the inlet and outlet of the gas passage to thethrough holes, the reactant gas or coolant is supplied to thecorresponding passage through one of the through holes and the surplusgas and reaction by-product or coolant is discharged through another oneof the through holes.

In the PEMFC, a plurality of the separation plates are stacked with oneanother and thus the through holes of the separation plates form asingle manifold. This is referred to as “an internal manifold type”.Instead of forming the through holes in the separator, a pipe fordispensing the gas or other structures may be installed on an outersurface of the separator. This is referred to as “an external manifoldtype”.

As described above, the conventional PEMFC includes a plurality ofstacked unit cells each having the membrane-electrode assembly and theanode and cathode separation plates disposed on the respective oppositesurfaces of the membrane-electrode assembly. The unit cells are coupledto each other by an appropriate compression force.

However, since the conventional PEMFC has a characteristic where ahydrogen ion conduction property thereof rises in proportion to anamount of moisture contained in the proton electrolyte membrane that isformed of a perfluorosulfonic acid-based material, the reactant gas,moisture of the proton electrolyte membrane, and heat must be properlycontrolled in order to obtain satisfactory performance thereof.

Particularly, when the PEMFC operates under a high load condition, theelectrochemical reaction increases and thus the amount of moisturegenerated from the cathode side increases. This disturbs the supply ofthe reactant gas to the electrode. This phenomenon is referred to as “aflooding phenomenon”. In addition, since the current density of theconventional PEMFC increases, the supply speed of the reactant gas islower than the electrochemical reaction speed. This causes an increaseof the concentration polarization phenomenon of the electrode.

Therefore, in order to solve the flooding phenomenon or the increase ofthe concentration polarization phenomenon, a method for reducing thereactant gas utilization rate has been usually used. That is, accordingto the method for reducing the reactant gas utilization rate, a flowrate of the reactant gas supplied to the fuel cell increases to increasethe supply speed of the reactant gas to the electrode, thereby reducingthe concentration polarization. In addition, in order to reduce thereactant gas utilization rate, a pressure difference between the inletand outlet of the passage of the separator increases to improve themoisture removal capability from the passage, thereby improving theflooding phenomenon.

Nevertheless, in the above-described methods, an amount of the reactantgas supplied is excessively greater than an amount of the reactant gasthat is required for the actual reaction. Therefore, since the fuel andoxidizing agent are excessively consumed, the efficiency of the stack isdeteriorated or the consumption of power for operating a compressorsupplying the reactant gas increases.

Therefore, in order to solve the flooding phenomenon and theconcentration polarization phenomenon, a method for increasing a channellength and reducing the number of channels of the passage formed on theseparator has also been used. However, this method has a problem in thatpressure loss occurs unnecessarily at a low load region where both ofthe flooding phenomenon and the concentration polarization phenomenon donot occur.

DISCLOSURE Technical Problem

The present invention has been made in an effort to solve theabove-described problems of the prior art. An object of the presentinvention is to provide a fuel cell separator that can suppress aflooding phenomenon and a concentration polarization phenomenon bycontrolling the supply of reactant gas in accordance with an operationcondition without excessive reactant gases, a fuel cell stack having theseparator, and a reactant gas control method of the fuel cell stack.

Technical Solution

In one exemplary embodiment, a fuel cell separator for supplyingreactant gases to a membrane-electrode assembly of a fuel cell stackincludes reactant gas inlet through holes for introducing reactantgases, and reactant gas outlet though holes for discharging the reactantgases, wherein the reactant gas inlet through holes and the reactant gasoutlet through holes are alternately formed along a first side edge ofthe fuel cell separator and one or more passages are formed on at leastone of opposite surfaces of the fuel cell separator to connect thereactant gas inlet through holes to the respective reactant gas outletthrough holes.

One of the reactant gases is an oxidizing gas, and a first oxidizingagent inlet through hole, a first oxidizing agent outlet through hole, asecond oxidizing agent inlet through hole, and a second oxidizing agentoutlet through hole are sequentially formed along an edge for theintroduction and exhaust of the oxidizing gas.

The reactant gas passages are oxidizing agent passages, and theoxidizing agent passages are formed on one of the opposite surfaces tointerconnect the oxidizing agent inlet through holes and the oxidizingagent outlet through holes such that a plurality of channels can be bentone time to form a U-shaped flow.

Alternatively, the reactant gas passages are oxidizing agent passages,and the oxidizing agent passages are formed on one of the oppositesurfaces to interconnect the oxidizing agent inlet through holes and theoxidizing agent outlet through holes such that a plurality of channelscan be bent at least two times to form a meander-shaped flow.

The other reactant gas is a fuel gas, and a first fuel inlet throughhole, a first fuel outlet through hole, a second fuel inlet throughhole, and a second fuel outlet through hole are sequentially formedalong an edge for the introduction and exhaust of the fuel gas.

The reactant gas passages are fuel passages, and the fuel passages areformed on one of the opposite surfaces to interconnect the fuel inletthrough holes and the fuel outlet through holes such that a plurality ofchannels can be bent one time to form a U-shaped flow.

Alternatively, the reactant gas passages are fuel passages, and the fuelpassages are formed on one of the opposite surfaces to interconnect thefuel inlet through holes and the fuel outlet through holes such that aplurality of channels can be bent at least two times to form ameander-shaped flow.

In another exemplary embodiment, a fuel cell stack includes: a pluralityof unit cells stacked with one another and each including amembrane-electrode assembly and a pair of separation plates; and endplates that are integrally coupled to opposite ends of the stacked unitcells by coupling members, respectively. The end plates are providedwith reactant gas inlet ports supplying reactant gases and correspondingto the reactant gas inlet through holes, and reactant gas outlet portsdischarging residual reactant gases and reaction by-product andcorresponding to the reactant gas inlet through holes, the reactant gasinlet ports and the reactant gas outlet ports being alternately formed.The end plates include valves, which are installed on pipes connectingthe reactant gas inlet ports to the reactant gas outlet ports to controlreactant gas flow.

One of the reactant gases is an oxidizing gas, and the end platesinclude a first end plate coupled to one end of the stacked unit cells.The reactant gas inlet ports are first and second oxidizing agent inletports for supplying the oxidizing gas, and the reactant gas outlet portsare first and second oxidizing agent outlet ports for dischargingresidual oxidizing gas and reaction by-product.

One of the valves is an oxidizing agent inlet valve, which is installedon a pipe interconnecting the first and second oxidizing agent inletports to control flow of the oxidizing gas.

One of the valves is an oxidizing agent outlet valve, which is installedon a pipe interconnecting the first and second oxidizing agent outletports to control flow of the oxidizing gas.

The end plates further include a second end plate coupled to the otherend of the stacked unit cells. The reactant gas inlet ports furtherinclude a third oxidizing agent inlet port sharing a manifold with thesecond oxidizing agent inlet port, and the reactant gas outlet portsfurther include a third oxidizing agent outlet port sharing a manifoldwith the first oxidizing agent outlet port.

The valves further include an oxidizing agent intermediate valve, whichis installed on a pipe interconnecting the third oxidizing inlet andoutlet ports to control oxidizing gas flow.

One of the reactant gases is a fuel gas, and the end plates include afirst end plate coupled to one end of the stacked unit cells. Thereactant gas inlet ports are first and second fuel inlet ports forsupplying the fuel gas and the reactant gas outlet ports are first andsecond fuel outlet ports for discharging residual fuel gas.

One of the valves is a fuel inlet valve, which is installed on a pipeinterconnecting the first and second fuel inlet ports to control flow ofthe fuel gas.

One of the valves is a fuel outlet valve, which is installed on a pipeinterconnecting the first and second fuel outlet ports to control flowof the fuel gas.

The end plates further include a second end plate coupled to the otherend of the stacked unit cells. The reactant gas inlet ports furtherinclude a third fuel inlet port sharing a manifold with the second fuelinlet port, and the reactant gas outlet ports further include a thirdfuel outlet port sharing a manifold with the first fuel outlet port.

The valves further include a fuel intermediate valve, which is installedon a pipe interconnecting the third fuel inlet and outlet ports tocontrol fuel gas flow.

In still another exemplary embodiment, a method of controlling reactantgas of the fuel cell stack includes determining if a performancedeterioration cause, such as a flooding phenomenon or concentrationpolarization phenomenon, occurs in the fuel cell stack. The methodfurther includes controlling, when it is determined that the performancedeterioration cause does not occur in the fuel cell stack, a reactantgas supply to the fuel cell stack in accordance with a low loadoperation condition, and, when it is determined that the performancedeterioration cause occurs in the fuel cell stack, the reactant gassupply to the fuel cell stack in accordance with a high load operationcondition. In the low load operation condition, the reactant gas inletvalve and the reactant gas outlet valve are opened and the reactant gasintermediate valve is closed so that the reactant gas is suppliedthrough the first and second reactant gas inlet ports and dischargedthrough the first and second reactant gas outlet ports. In the high loadoperation condition, the reactant gas inlet valve and the reactant gasoutlet valve are closed and the reactant gas intermediate valve isopened so that the reactant gas is supplied only through the firstreactant gas inlet port and discharged only through the second reactantgas outlet port.

The reactant gas flow is an oxidizing gas flow. In the low loadoperation condition, the oxidizing gas is supplied through the first andsecond oxidizing agent inlet ports. Then, the oxidizing gas passes alongan oxidizing agent inlet manifold formed by the stack unit cells, in thecourse of which the oxidizing gas is introduced into the oxidizing agentpassages through the first and second oxidizing agent inlet throughholes. Next, the oxidizing gas is used for an electrochemical reaction,after which the oxidizing gas is discharged to the oxidizing agentoutlet manifolds through the first and second oxidizing agent outletthrough holes to be finally discharged to an external side through thefirst and second oxidizing agent outlet ports.

In the high load operation condition, the oxidizing gas is supplied onlyto the first oxidizing agent inlet port. Then, the oxidizing gas passesalong the oxidizing agent inlet manifold formed by the stacked unitcells, in the course of which the oxidizing gas is introduced into thefirst oxidizing agent passage through the first oxidizing agent inletthrough hole. Next, the oxidizing gas is used for the electrochemicalreaction, after which the oxidizing gas is directed to the thirdoxidizing agent outlet port through the first oxidizing agent outletmanifold and the first oxidizing agent outlet through hole, andintroduced again to the second oxidizing agent inlet manifold throughthe third oxidizing agent inlet port. Next, the oxidizing gas isintroduced into the second oxidizing agent passage through the secondoxidizing inlet through hole of the fuel cell separator. The oxidizinggas is used again for the electrochemical reaction, discharged to thesecond oxidizing agent outlet manifold through the second oxidizingagent outlet through hole, directed to the second oxidizing agent outletport, and finally discharged to the external side through the secondoxidizing agent outlet port.

The reactant gas flow is a fuel gas flow. In the low load operationcondition, the fuel gas is supplied through the first and second fuelinlet ports. Then, the fuel gas passes along a fuel inlet manifoldformed by the stacked unit cells, in the course of which the fuel gas isintroduced into the fuel passages through the first and second fuelagent inlet through holes. Next, the fuel gas is used for anelectrochemical reaction, after which the fuel gas is discharged to thefuel outlet manifolds through the first and second fuel outlet throughholes to be finally discharged to an external side through the first andsecond fuel outlet ports.

In the high load operation condition, the fuel gas is supplied only tothe first fuel inlet port. The fuel gas passes along the first fuelinlet manifold formed by the stacked unit cells, in the course of whichthe fuel gas is introduced into the first fuel passage through the firstfuel inlet through hole. Next, the fuel gas is used for theelectrochemical reaction, after which the fuel gas is discharged to thefirst fuel outlet manifold through the first fuel outlet through hole,directed to the third fuel outlet port, and introduced again to thesecond fuel inlet manifold through the third fuel inlet port. After theabove, the fuel gas is introduced into the second fuel passage throughthe second fuel inlet through hole of the fuel cell separator. Next, thefuel gas is used again for the electrochemical reaction, discharged tothe second fuel outlet manifold through the second fuel outlet throughhole, and finally discharged to the external side through the secondfuel outlet port.

Advantageous Effects

According to the present invention, by controlling the reactant gassupply in accordance with an operation condition of the fuel cell stackwithout experiencing pressure loss and deterioration of the utilizingrate, the flooding phenomenon and concentration polarization phenomenonthat occur in the fuel cell stack can be prevented.

DESCRIPTION OF DRAWINGS

FIG. 1 is a front view of a fuel cell separator according to a firstexemplary embodiment of the present invention.

FIG. 2 is a front view of a fuel cell separator according to a secondexemplary embodiment of the present invention.

FIG. 3 is an exploded perspective view of a fuel cell stack having thefuel cell separator of FIG. 1 or FIG. 2 according to an exemplaryembodiment of the present invention, illustrating oxidizing gas flow ina low load operation.

FIG. 4 is a schematic diagram illustrating oxidizing gas flow in thefuel cell separator of FIG. 3 in a low load operation.

FIG. 5 is an exploded perspective view of the fuel cell stack of FIG. 3,illustrating oxidizing gas flow in a high load operation.

FIG. 6 is a schematic diagram illustrating oxidizing gas flow in thefuel cell separator of FIG. 3 in a high load operation.

FIG. 7 is an exploded perspective view of the fuel cell stack of FIG. 3,illustrating fuel gas flow in a low load operation.

FIG. 8 is an exploded perspective view of the fuel cell stack of FIG. 3,illustrating fuel gas flow in a high load operation.

FIG. 9 is an exploded perspective view of the fuel cell stack of FIG. 3,illustrating coolant flow.

DESCRIPTION OF REFERENCE NUMERALS INDICATING PRIMARY ELEMENTS IN THEDRAWINGS

100, 101, 102, 104, 105: Separation Plate

200: Fuel Cell Stack

210: Unit cell

220, 230: End Plate

221, 223, 231: Oxidizing Inlet Port

222, 224, 232: Oxidizing Outlet Port

225: Oxidizing Agent Inlet Valve

226: Oxidizing Agent Outlet Valve

235: Oxidizing Agent Intermediate Valve

251, 253, 261: Fuel Inlet Port

252, 254, 262: Fuel Outlet Port

255: Fuel Inlet Value

256: Fuel Outlet Valve

265: Fuel Intermediate Value

BEST MODE

The present invention will be described more fully hereinafter withreference to the accompanying drawings, in which exemplary embodimentsof the invention are shown. As those skilled in the art would realize,the described embodiments may be modified in various different ways, allwithout departing from the spirit or scope of the present invention.

FIG. 1 is a front view of a fuel cell separator according to a firstexemplary embodiment of the present invention.

The fuel cell separator of the first exemplary embodiment may be dividedinto a cathode separation plate and an anode separation plate inaccordance with a reactant gas. However, the cathode and anodeseparation plates have the following identical features. As shown inFIG. 1, a cathode separation plate 100 is provided with a firstoxidizing agent inlet through hole 111, a first oxidizing agent outletthrough hole 112, a second oxidizing agent inlet through hole 113, and asecond oxidizing agent outlet rough hole 114. The first oxidizing agentinlet through hole 111, the first oxidizing agent outlet through hole112, the second oxidizing agent inlet through hole 113, and the secondoxidizing agent outlet through hole 114 are formed along a first sideedge of the cathode separation plate 100 to allow the oxidizing agent tobe introduced and discharged. A first oxidizing agent passage 121 isformed on a first surface of the cathode separation plate 100 to connectthe first oxidizing agent inlet through hole 111 to the first oxidizingagent outlet through hole 112 such that a plurality of channels can bebent one time to form a U-shaped flow. A second oxidizing agent passage122 is formed on the cathode separation plate 100 to connect the secondoxidizing agent inlet through hole 113 to the second oxidizing agentoutlet through hole 114 such that a plurality of channels can be bentone time to form a U-shaped flow.

The first oxidizing agent inlet through hole 111, the first oxidizingagent outlet through hole 112, the second oxidizing agent inlet throughhole 113, and the second oxidizing agent outlet through hole 114 areformed along the first side edge of the cathode separation plate 100.The cathode separation plate 100 is provided with a first fuel inletthrough hole 131, a first fuel outlet through hole 132, a second fuelinlet through hole 133, and a second fuel outlet through hole 134. Thefirst fuel inlet through hole 131, the first fuel outlet through hole132, the second fuel inlet through hole 133, and the second fuel outletthrough hole 134 are formed along a second side edge of the cathodeseparation plate 100, which is opposite to the first side, to allow thefuel to be introduced and discharged. At this point, the first fuelinlet through hole 131 is disposed not to face the first oxidizing agentinlet through hole 111 but rather is diagonally disposed with respect tothe first oxidizing agent inlet through hole 111. However, the presentinvention is not limited to this configuration. That is, the first fuelinlet through hole 131 may be disposed to face the first oxidizing agentinlet through hole 111.

A first fuel passage is formed on a first surface of the anodeseparation plate to connect the first fuel inlet through hole 131 to thefirst fuel outlet through hole 132 such that a plurality of channels canbe bent one time to form a U-shaped flow of the fuel. A second fuelpassage is formed on the anode separation plate to connect the secondfuel inlet through hole 133 to the second fuel outlet through hole 134such that a plurality of channels can be bent one time to form aU-shaped flow of the fuel.

The cathode separation plate 100 and the anode separation plate areprovided with a coolant inlet through hole 141 and a coolant outletthrough hole 142. The coolant inlet and outlet through holes 141 and 142are respectively formed on opposite edges on which the oxidizing inletthrough holes 111 and 113, the oxidizing outlet through holes 112 and114, the fuel inlet through holes 131 and 133, and the fuel outletthrough holes 132 and 134 are not formed. The coolant inlet through hole141 and the coolant outlet through hole 142 are interconnected by acoolant passage formed on second surface of the fuel cell separator.

Further, the cathode separation plate 100 may be assembled with theanode separation plate such that the coolant passage forming surface ofthe cathode separation plate 100 faces the coolant passage formingsurface of the anode separation plate. Alternatively, the cathodeseparation plate 100 may be assembled with the anode separation platesuch that the coolant passage forming surface of the cathode separationplate 100 faces a surface of the anode separation plate, on which thecoolant passage is not formed.

Although the cathode separation plate 100 and the anode separation plateare designed such that the oxidizing agent passages 121 and 122 and thefuel passages are formed to have U-shaped flows, the present inventionis not limited to this configuration. That is, as shown in FIG. 2, eachof the passages may be formed such that the plurality of channels arebent two or more times to form a meander-shaped flow.

The following will describe a fuel cell stack having the above-describedfuel cell separator and a method of controlling a reactant gas(oxidizing gas and fuel gas) used in the fuel cell stack.

FIG. 3 is an exploded perspective view of a fuel cell stack having thefuel cell separator of FIG. 1 or FIG. 2 according to an exemplaryembodiment of the present invention, illustrating oxidizing gas flow ina low load operation.

As shown in FIG. 3, a fuel cell stack 200 of the present exemplaryembodiment uses the fuel cell separator having the cathode separationplate 100 and the anode separation plate. That is, the fuel cell stack200 includes a plurality of unit cells 210 (only one is shown in FIG. 3)stacked with one another. Each of the unit cells 210 includes a fuelcell separator having a cathode separation plate 101 and an anodeseparation plate 102, and a membrane-electrode assembly 103. At thispoint, separation plates that are located on outermost ends of thestacked unit cells 210 will be referred to as a longitudinal end cathodeseparation plate 104 and a longitudinal end anode separation plate 105,respectively. Since the longitudinal anode and cathode separation plates105 and 104 contact respectively first and second end plates 220 and230, inner surfaces of the longitudinal cathode and anode separationplates 104 and 105 are provided with an oxidizing agent passage or afuel passage and outer surfaces are not provided with any passage. Thefirst and second end plates 220 and 230 are located on opposite ends ofa body formed by the stacked unit cells 210 and are integrally coupledto the body by coupling members (not shown).

The first end plate 220 is provided with first and second oxidizingagent inlet ports 221 and 223 for supplying the oxidizing gas, and firstand second oxidizing agent outlet ports 222 and 224 for dischargingresidual oxidizing gas that is not used for the electrochemical reactionand reaction by-product. A first pipe for interconnecting the first andsecond oxidizing agent inlet ports 221 and 223 is installed on the firstend plate 220, and an oxidizing agent inlet valve 225 for selectivelychecking the gas flow at a portion near a front end of the secondoxidizing agent inlet port 223 is installed on the first pipe. Further,a second pipe for interconnecting the first and second oxidizing agentoutlet ports 222 and 224 is installed on the first end plate 220, and anoxidizing agent outlet valve 226 for selectively checking the gas flowat a portion near a front end of the second oxidizing agent outlet port222 is installed on the second pipe.

The second end plate 230 is further provided with a third oxidizinginlet port 231 sharing a manifold with the second oxidizing agent inletport 223 and a third oxidizing agent outlet port 232 sharing a manifoldwith the first oxidizing agent outlet port 222. Further, a third pipefor interconnecting the third oxidizing agent inlet and outlet ports 231and 232 is installed on the second end plate 230, and an oxidizing agentintermediate valve 235 for selectively checking the gas flow at aportion near a front end of the third oxidizing agent inlet port 231 isinstalled on the third pipe.

The flow of the oxidizing gas in the low load operation of the fuel cellstack 200 is controlled by the following process. In the low loadoperation condition of the fuel cell stack 200, the oxidizing agentinlet valve 225 and the oxidizing agent outlet valve 226 are opened andthe oxidizing agent intermediate valve 235 is closed.

Then, as shown in FIGS. 1 and 3, the oxidizing gas is uniformly suppliedto the first and second oxidizing agent inlet ports 221 and 223. Theoxidizing gas passes through an oxidizing agent inlet manifold 240formed by stacking the unit cells 210, in the course of which theoxidizing gas is introduced into the oxidizing agent passages 121 and122 through the respective first and second oxidizing agent inletthrough holes 111 and 113. The oxidizing gas is used for theelectrochemical reaction, after which it is discharged to the oxidizingagent outlet manifold 242 through the first and second oxidizing agentoutlet through holes 112 and 114. At this point, since the oxidizingagent intermediate valve 235 is closed, the oxidizing gas is dischargedto an external side through the first and second oxidizing agent outletports 222 and 224.

That is, even when the fuel cell stack 200 operates under the low loadoperation condition, as shown in FIG. 4, the oxidizing gas is suppliedto the oxidizing agent passages 121 and 122 of the cathode separationplate 100, and thus, the length of the passage can be shortened by 50%as compared with the prior art having only one oxidizing agent passage.Therefore, the reactant gas can be effectively supplied withoutexperiencing pressure loss.

FIG. 5 is an exploded perspective view of the fuel cell stack of FIG. 3,illustrating oxidizing gas flow in a high load operation.

In a high load operation of a conventional fuel cell stack, since acurrent density is high, the flooding phenomenon may occur and theconcentration polarization increases. To solve this problem, the flowrate and pressure in the passages should be significantly increased byreducing the reactant gas utilizing rate. However, in the presentexemplary embodiment, the oxidizing gas flow can be controlled by thefollowing process without lowering the reactant gas utilizing rate inthe high load operation and employing a separation plate only for thehigh load operation.

That is, as shown in FIGS. 1 and 5, in a high load operation condition,the oxidizing agent inlet and outlet valves 225 and 226 are closed andthe oxidizing agent intermediate valve 235 is opened.

Then, the oxidizing gas is supplied through only the first oxidizingagent inlet port 221. The oxidizing gas passes through an oxidizingagent inlet manifold 240, in the course of which the oxidizing gas isintroduced into the oxidizing agent passages 121 through the firstoxidizing agent inlet through holes 111. The oxidizing gas is used forthe electrochemical reaction, after which it is discharged to theoxidizing agent outlet manifold 242 through the first oxidizing agentoutlet through holes 112 and subsequently directed to the thirdoxidizing agent outlet port 232. The oxidizing gas directed to the thirdoxidizing agent outlet port 232 is introduced into the second oxidizingagent inlet manifold 241 through the third oxidizing agent inlet port231, after which it is directed to the second oxidizing agent passages122 through the second oxidizing agent inlet through holes 113 of thecathode separation plates 100. Then, the oxidizing gas is used again forthe electrochemical reaction, after which it is discharged to the secondoxidizing agent outlet manifold 243 through the second oxidizing agentoutlet through holes 114 and subsequently discharged to the externalside through the second oxidizing agent outlet port 224.

As described above, in the high load operation of the fuel cell stack200, as shown in FIG. 6, the oxidizing gas is introduced into the firstoxidizing agent passage 121 of the cathode separation plate 100 andutilized in half of the whole electrode area. Subsequently, theoxidizing gas is introduced into the second oxidizing passage 122 andutilized in the remaining half of the electrode area. Further, in thehigh load operation of the fuel cell stack 200, since the oxidizing gasis supplied through only one oxidizing agent inlet port, the flow rateof the oxidizing gas flowing along the passage channels is increased bytwo times, even when the reactant gas utilizing rate is identical ascompared with the oxidizing gas flow in the low load operation of FIG.3. As a result, according to the fuel cell stack 200 of the presentexemplary embodiment, the moisture existing in the passage channels canbe more effectively discharged and the flooding phenomenon occurring inthe high load operation can be prevented. Further, according to thereactant gas 5 control method of the fuel cell stack 200, since thesupply speed of the oxidizing gas to the passage channels in the highload operation is increased, an amount of the reactant gas supplied tothe electrode increases and thus the concentration polarizationphenomenon can be reduced.

As a result, the reactant gas control method of the fuel cell stack 200controls the oxidizing gas flow using a method identical to that for thelow load operation condition in a normal operation. Meanwhile, accordingto the reactant gas control method of the fuel cell stack 200, when theflooding phenomenon that causes the deterioration of the performance ofthe fuel cell stack occurs or the concentration polarization that alsocauses the deterioration of the performance of the fuel cell stackincreases, the oxidizing gas flow changes to a gas flow for the highload operation condition. When the performance deterioration causes aresolved, the oxidizing gas flow changes to a gas flow for the low loadoperation condition.

FIG. 7 is an exploded perspective view of the fuel cell stack of FIG. 3,illustrating fuel gas flow in a low load operation.

As shown in FIG. 7, the fuel cell stack 200 uses the fuel cell separatorof FIG. 1 or FIG. 2 and further includes additional constituent elementsthat will be described hereinafter to utilize the fuel gas.

The first end plate 220 is provided with first and second fuel inletports 251 and 253 for supplying the fuel gas, and first and second fueloutlet ports 252 and 254 for discharging residual fuel gas that is notused for the electrochemical reaction. A fourth pipe for interconnectingthe first and second fuel inlet ports 251 and 253 is installed on thefirst end plate 220, and a fuel inlet valve 255 for selectively checkingthe gas flow at a portion near a front end of the second fuel inlet port253 is installed on the fourth pipe. Further, a fifth pipe forinterconnecting the first and second fuel outlet ports 252 and 254 isinstalled on the first end plate 220, and a fuel outlet valve 256 forselectively checking the gas flow at a portion near a front end of thesecond fuel outlet port 252 is installed on the fifth pipe.

The second end plate 230 is further provided with a third fuel inletport 261 sharing a manifold with the second fuel inlet port 253 and athird fuel outlet port 262 sharing a manifold with the first fuel outletport 252. Further, a sixth pipe for interconnecting the third fuel inletand outlet ports 261 and 262 is installed on the second end plate 230,and a fuel intermediate valve 265 for selectively checking the gas flowat a portion near a front end of the third fuel inlet port 261 isinstalled on the sixth pipe.

As described above, the constituent elements for utilizing the fuel gasare similar to those for utilizing the oxidizing gas.

Therefore, the fuel is uniformly supplied to the first and second fuelinlet ports 251 and 253. The fuel passes through a fuel inlet manifold270, in the course of which the fuel gas is introduced into the fuelpassages of the anode separation plates. Next, the fuel is used for theelectrochemical reaction, after which it is discharged to the fueloutlet manifold 272. At this point, since the fuel intermediate valve265 is closed, the fuel is subsequently discharged to the external sidethrough the first and second fuel outlet ports 252 and 254.

In the fuel cell stack 200, the oxidizing agent inlet through holes 111and 113 and the oxidizing agent outlet through holes 112 and 114 areoppositely located with respect to the fuel inlet through holes 131 and133 and the fuel outlet through holes 132 and 134. However, although thefuel gas flow and the oxidizing gas flow are different in a verticallocation from each other, the operation control methods thereof areidentical to each other.

FIG. 8 is an exploded perspective view of the fuel cell stack of FIG. 3,illustrating fuel gas flow in a high load operation.

As shown in FIGS. 1 and 8, the fuel gas is supplied through only thefirst fuel inlet port 251. The fuel gas passes through the fuel inletmanifold 270, in the course of which the fuel gas is introduced into thefuel passages through the first fuel inlet through holes 131. The fuelis used for the electrochemical reaction, after which it is dischargedto the fuel outlet manifold 272 through the first fuel outlet throughholes 132 and subsequently directed to the third fuel outlet port 262.The fuel directed to the third fuel outlet port 262 is introduced intothe second fuel inlet manifold 271 through the third fuel inlet port261, after which it is directed to the second fuel passages through thesecond fuel inlet through holes 133. Then, the fuel gas is used againfor the electrochemical reaction, after which it is discharged to thesecond fuel outlet manifold 273 through the second fuel outlet throughholes 134 and subsequently discharged to the external side through thesecond fuel outlet port 254.

As described above, the method for controlling the oxidizing gas flow isidentically applied to the method for controlling the fuel gas flow.

FIG. 9 is an exploded perspective view of the fuel cell stack of FIG. 3,illustrating coolant flow.

As shown in FIGS. 1 and 9, one of the first and second end plates 220and 230 (the first end plate 220 in the drawing) is provided with acoolant inlet port 280 for supplying a coolant and a coolant outlet port281 for discharging the coolant. Then, the coolant is introduced intothe fuel cell stack 200 through the coolant inlet port 280 and flowsalong the coolant passage through the coolant inlet through holes 141formed in the fuel cell separators to cool the fuel cell stack 200,after which it is discharged to the external side through the coolantoutlet port 281. At this point, the coolant flows in the fuel cellseparators in a direction in which the oxidizing gas flows. That is, ifthe oxidizing gas flows upward, the coolant may also flow upward.

As described above, the fuel cell separator of the present exemplaryembodiment is provided with a pair of the oxidizing agent passages 121and 122 and a pair of the fuel passages to charge respective dividedregions of the whole electrode area. However, the present invention isnot limited to this configuration. That is, two or more pairs of theoxidizing agent passages and two or more pairs of the fuel passages maybe formed. In this case, additional constituent elements for supplyingand discharging the oxidizing gas and fuel gas to and from the fuel cellseparator may be further provided.

While this invention has been described in connection with what ispresently considered to be practical exemplary embodiments, it is to beunderstood that the invention is not limited to the disclosedembodiments, but, on the contrary, is intended to cover variousmodifications and equivalent arrangements included within the spirit andscope of the appended claims.

What is claimed is:
 1. A fuel cell separator for supplying reactant gasto a membrane-electrode assembly of a fuel cell stack, the fuel cellseparator comprising: reactant gas inlet through holes for introducingreactant gases; reactant gas outlet though holes for discharging thereactant gases; and a coolant inlet through hole for introducing acoolant; and a coolant outlet through hole for discharging the coolant,wherein the reactant gas inlet through holes and the reactant gas outletthrough holes are alternately formed along an edge of the fuel cellseparator and one or more passages are formed on at least one ofopposite surfaces of the fuel cell separator to connect the reactant gasinlet through holes to the respective reactant gas outlet through holes,wherein one of the reactant gases is an oxidizing gas, and a firstoxidizing agent inlet through hole, a first oxidizing agent outletthrough hole, a second oxidizing agent inlet through hole, and a secondoxidizing agent outlet through hole are sequentially formed along afirst side edge of the fuel cell separator, for an introduction andexhaust of the oxidizing gas, wherein one of the reactant gases is afuel gas, and a first fuel inlet through hole, a first fuel outletthrough hole, a second fuel inlet through hole, and a second fuel outletthrough hole are sequentially formed along a second side edge of thefuel cell separator, which is opposite to the first side edge, for anintroduction and exhaust of the fuel gas, wherein the coolant inletthrough hole and the coolant outlet through hole are respectively formedon opposite edges of the full cell separator on which the reactant gasinlet through holes and the reactant gas outlet though holes are notformed, and wherein the coolant flows in a direction in which theoxidizing gas flows.
 2. The fuel cell separator of claim 1, wherein thereactant gas passages are oxidizing agent passages, and the oxidizingagent passages are formed on one of the opposite surfaces tointerconnect the oxidizing agent inlet through holes and the oxidizingagent outlet through holes such that a plurality of channels can be bentone time to form a U-shaped flow.
 3. The fuel cell separator of claim 1,wherein the reactant gas passages are oxidizing agent passages, and theoxidizing agent passages are formed on one of the opposite surfaces tointerconnect the oxidizing agent inlet through holes and the oxidizingagent outlet through holes such that a plurality of channels can be bentat least two times to form a meander-shaped flow.
 4. The fuel cellseparator of claim 1, wherein the reactant gas passages are fuelpassages, and the fuel passages are formed on one of the oppositesurfaces to interconnect the fuel inlet through holes and the fueloutlet through holes such that a plurality of channels can be bent onetime to form a U-shaped flow.
 5. The fuel cell separator of claim 1,wherein the reactant gas passages are fuel passages, and the fuelpassages are formed on one of the opposite surfaces to interconnect thefuel inlet through holes and the fuel outlet through holes such that aplurality of channels can be bent at least two times to form ameander-shaped flow.